Through-air dryer assembly

ABSTRACT

A through-air dryer is disclosed. The through-air dryer includes a cylindrical deck made from a plurality of deck plates that support a throughdrying fabric. The deck plates are supported by opposing hubs. Each of the hubs is in communication with a bearing that is mounted to a stationary shaft for allowing the cylindrical deck and the hubs to rotate. The bearings are positioned so as to create a through-air dryer structure that remains stable during operation and allows for easy calculation of loads on the dryer.

BACKGROUND OF THE INVENTION

In the manufacture of high-bulk tissue products, such as facial tissue,bath tissue, paper towels, and the like, it is common to use one or morethrough-air dryers for partially drying the web or to bring the tissueweb to a final dryness or near-final dryness. Generally speaking,through-air dryers typically include a rotating cylinder having an upperdeck that supports a drying fabric which, in turn, supports the webbeing dried. In particular, heated air is passed through the web inorder to dry the web. For example, in one embodiment, heated air isprovided by a hood above the drying cylinder. Alternatively, heated airis provided to a center area of the drying cylinder and passed throughto the hood.

When incorporated into a papermaking system, through-air dryers offermany and various benefits and advantages. For example, through-airdryers are capable of drying tissue webs without compressing the web.Thus, moisture is removed from the webs without the webs losing asubstantial amount of bulk or caliber. In fact, through-air dryers, insome applications, may even serve to increase the bulk of the web.Through-air dryers are also known to contribute to various otherimportant properties and characteristics of the webs.

Through-air dryers, however, are typically much more expensive tomanufacture and ship in comparison to other drying devices. Forinstance, many conventional through-air dryers include a rotatingcylindrical deck that is made from a single piece construction. In orderto permit air flow, the cylindrical deck is porous. Further, in order tosupport the significant loads that are exerted on the deck duringoperation, the cylindrical deck has a substantial thickness. In thepast, the decks have been made from expensive materials, such asstainless steel, and have been manufactured using expensive procedures.For instance, in order to make the decks porous, the decks are typicallyconfigured to have a honeycomb-like structure that requires asubstantial amount of labor intensive and critical welding. In order tosupport the cylindrical deck and to control air flow through the deck,many through-air dryers also include internal baffles and seals thatfurther increase the cost of the equipment.

Further, since the cylindrical deck is a one-piece construction, theshipping costs for through-air dryers are exorbitant. For example, sincethe decks cannot be disassembled, specially designed shippingarrangements usually are required.

Recently, demands have been made to increase the capacity and efficiencyof through-air dryers. As such, gas flow rates through the dryers haveincreased. In order to shield the bearings that allow the dryers torotate from the gas flow path, the bearings have been shifted inposition. For instance, referring to FIG. 1, a simplified diagram of aprior art through-air dryer is illustrated. As shown, the through-airdryer includes a cylindrical deck 1 that is supported by a pair ofopposing heads 2. The heads 2 are mounted on a rotating shaft 3.

The through-air dryer further includes a pair of bearings 4. Thebearings 4 allow for the shaft 3 to rotate. In order to prevent thebearings from being exposed to the hot gas flow traveling through thethrough-air dryer, the bearings are typically spaced a significantdistance from the heads 2. Unfortunately, as a result of the placementof the bearings 4, moments represented by the arrows 5 are created whena load 6 is placed on the through-air dryer during operation. Themoments need to be supported by the shaft 3, the heads 2, and thecylindrical deck 1. Thus, due to the presence of the moments, evengreater deck thicknesses and massive heads are required in designing thethrough-air dryer, further increasing the cost to manufacture the dryerand the cost to ship the dryer. An added problem with the existingdesign is that significant stresses are caused by the differentialexpansion of components during the heating of the through-air dryer andby the differential temperatures of the through-air dryer duringsteady-state operation. The safest way to start up a traditionalthrough-air dryer is to limit the warm up rate to a few degrees perminute to allow all parts to equilibrate to the same temperature. Thissubjects the dryer to lowest differential loads, but there are alwaysstresses induced with a rigid design. Another method to limit the effectof differential expansion from temperature is by the use of exoticmaterials that have different rates of thermal expansion. For example,the deck, which is typically thin and heats up faster that the supportstructure, can be made from a material that has a lower coefficient ofthermal expansion. This net thermal expansion rate between the deck andsupport structure is more similar reducing stress. While this helps toalleviate the problem, the cost of the through-air dryer is much higherbecause of the expense of special materials and the special machiningand handling necessary to weld them.

As such, a need currently exists for a through-air dryer design that issimple to produce, controls the loads and moment on the structure, iseasy to ship and is not practically limited in size. A need also existsfor a through-air dryer design that has a lower capital cost and may bedisassembled for facilitating construction and shipping of the dryer. Aneed also exists for a through-air dryer design that does not createhigh moments that must be supported by the dryer structure.

SUMMARY OF THE INVENTION

In general, the present invention is directed to an apparatus forthrough-air drying webs. The through-air dryer of the present inventionis capable of being disassembled and is therefore easy to ship. Thethrough-air dryer is also capable of accommodating all different sizes,and may, for instance, be built to have large diameters. Further, thethrough-air dryer is configured so that no significant moments arepresent in the head or shell from outboard placement of bearings andsupports, thereby lessening the structural demands of the device. Theuse of simple plates to form the deck makes it relatively simple tocalculate loads that are exerted on the dryer.

For example, in one embodiment, the apparatus of the present inventionincludes a cylindrical deck having sufficient open space to permitairflow therethrough. A support structure is positioned to support thecylindrical deck. The apparatus further includes a support shaftconcentrically positioned with respect to the cylindrical deck. Thesupport structure is configured to rotate on the support shaft. At leastone bearing is positioned between the support shaft and the supportstructure to permit rotation of the support structure. The bearing islocated so that there is substantially no moment transfer between thecylindrical deck and the support structure.

The support structure, for example, may comprise a first hub spaced froma second hub. Each hub engages an opposite end of the cylindrical deck.A first bearing is positioned between the first hub and the supportshaft and a second bearing is positioned between the second hub and thesupport shaft. Each bearing is placed substantially in alignment witheach end of the cylindrical deck in order to prevent the creation ofmoment from the offset of the location of the load relative to thelocation of support. The alignment of the bearing in the supportstructure eliminates the moment that the deck is required to carry sothat the deck can be designed for fabric load, rotational accelerationand pressure differential alone.

In one particular embodiment, the support structure may include arotating tube surrounding the support shaft. The rotating tube isconnected at a first end to the first hub and at a second end to thesecond hub. The rotating tube may be used to serve as a shield for thebearings so that the hot gas flow traveling through the dryer does notcontact the bearings.

It is recognized that temperature-controlled circulating oil will berequired to control the temperature of the bearing during operation.Temperature control is commonly done for circulating oil to control theviscosity of the oil to provide the correct hydrodynamic properties toensure separation of the metallic elements within the bearing. Bearingcooling is similar to that already done for steam-heated Yankee dryingcylinders where steam at elevated temperatures is fed through a shaftwhich in turn is supported by bearings. Temperature rise from heattransfer of the steam to the shaft and ultimately to the bearing iscontrolled by oil temperature.

The support structure can further include a first internal deck supportand a second internal deck support that extend between the rotating tubeand the cylindrical deck. A deck support ring supporting the cylindricaldeck in between the first end of the deck and the second end of the deckmay be connected to each of the internal deck supports.

The deck itself may comprise a plurality of individual deck plates thatare attached to the support structure. For instance, the deck plates maybe attached to the support structure using a pin attachment structurethat permits thermal expansion. If desired, the deck plates may have across sectional profile that tapers in a direction opposite thedirection of gas flow through the cylindrical deck. A hot gas, forexample, may travel from an exterior surface of the cylindrical deck toan interior space of the dryer. In an alternative embodiment, however,the gas may flow from inside the cylindrical deck to outside thecylindrical deck. In either instance, a hood may surround thecylindrical deck for directing the hot gas stream either into the deckor away from the deck.

For gas flow into the dryer it is advantageous to limit the width of thedeck plate as it contacts the web to reduce the tendency to cause sheetmarking. It has been found that a contact width of less than 3 mm (1/8inches) is preferable to prevent sheet marking. This thickness isdependent on the thickness of the fabric. For example, thicker morethree dimensional fabrics allow flow in the machine direction so markingwould be less noticeable. The location of internal supports is alsoideally located away from direct contact with the fabric to facilitateair flow.

In order to dry a web, the web may be carried on a throughdrying fabricthat is wrapped around the cylindrical deck. The throughdrying fabricmay be wrapped around the cylindrical deck from an upstream point to adownstream point leaving an open free end. In this embodiment, theapparatus may further include an external baffle positioned over theopen free end of the cylindrical deck for shielding the open free endfrom external air.

In accordance with the present invention, the cylindrical deck and thesupport structure may be made from multiple parts that may be easilyassembled. For instance, as described above, the cylindrical deck ismade from a plurality of plates. In addition, the support structure mayinclude opposing hubs that also may be comprised of multiple parts. Inthis manner, when the apparatus is being shipped, the shipping volume ofthe apparatus may have a greatest dimension of no greater than one halfthe diameter of the cylindrical deck.

Other features and aspects of the present invention are discussed ingreater detail below.

BRIEF DESCRIPTION OF THE DRAWINGS

A full and enabling disclosure of the present invention, including thebest mode thereof to one skilled in the art, is set forth moreparticularly in the remainder of the specification, including referenceto the accompanying figures, in which:

FIG. 1 is a cross sectional view of a through-air dryer showingconventional placement of bearings that cause the creation of moments inthe structure;

FIG. 2 is a side view of one embodiment of a tissue making processincorporating a through-air dryer made in accordance with the presentinvention;

FIG. 3 is a cross sectional view of one embodiment of a through-airdrying device in accordance with the present invention;

FIG. 3A is a cross sectional view of a single plate connection inaccordance with one embodiment of the present invention;

FIG. 4 is a partial side view of the through-air dryer illustrated inFIG. 3;

FIG. 5 is a side view of the through-air dryer shown in FIG. 3;

FIG. 6 is a diagrammatical view of a through-air dryer in accordancewith the present invention; and

FIGS. 7-10 are demonstrative figures used for calculating loads onthrough-air dryers made in accordance with the present invention as isexplained in the examples.

Repeated use of reference characters in the present specification anddrawings is intended to represent the same or analogous features orelements of the invention.

DETAILED DESCRIPTION OF THE INVENTION

It is to be understood by one of ordinary skill in the art that thepresent discussion is a description of exemplary embodiments only, andis not intended as limiting the broader aspects of the presentinvention.

In general, the present invention is directed to a through-air dryingapparatus, which passes a heated gas through a web in order to dry theweb. The through-air drying apparatus has multiple and numerousapplications. For example, in one embodiment, the apparatus may be usedfor drying a tissue web. It is also recognized that the same principlesof design can be used for smaller rolls typically used for vacuum orpressure transfer of the web between sections of a paper machine.

The through-air dryer of the present invention, in one embodiment, ismade from multiple components that may be easily assembled and/ordisassembled. In this manner, not only is the through-air dryerrelatively inexpensive to manufacture, but also may be shipped withoutany significant difficulties or added expense.

Of particular advantage, due to the ability to vary the size of thedryer, due to the close spacing of the bearing centers, and due to lowercapital costs, the through-air dryer of the present invention is wellsuited to being incorporated into existing tissue making lines that donot currently include a through-air dryer. For instance, the through-airdryer of the present invention is well suited to replacing a Yankeedryer or other similar drum drying device for improving the propertiesof tissue webs produced on the line. Machines that currently have aYankee dryer are generally limited in available room outside the machineframes and machine frames are relatively narrow. The short distancebetween bearing centers makes a dryer of this design particularlyadvantageous for this application.

In one embodiment of the present invention, the through-air dryer ismade in a manner such that no significant moment transfers occur betweenmajor components of the structure of the dryer. For instance, thebearings that support rotation of the dryer may be substantially alignedwith each end of a rotating drying cylinder. In this manner, loadsapplied to the dryer are supported in a more stable manner preventingmoment between sections.

Although the through-air dryer may be used in multiple and numerousapplications, as described above, in one embodiment, the through-airdryer is particularly well suited for use in the manufacture of tissuewebs. It is also recognized that the same principles of design can beused for smaller rolls typically used for vacuum or pressure transfer ofthe web between sections of a paper machine.

For purposes of illustration, for instance, one embodiment of apapermaking process made in accordance with the present invention isshown in FIG. 2. As illustrated, the system includes a head box 10 whichinjects and deposits a stream of an aqueous suspension of papermakingfibers between a first forming fabric 12 and a second forming fabric 14.The forming fabric 14 serves to support the newly-formed wet web 16downstream in the process as the web is partially dewatered to aconsistency of about 10 dry weight percent. Additional dewatering of thewet web 16 can be carried out, such as by vacuum suction, using one ormore vacuum boxes 18. As shown, the vacuum box 18 is positioned belowthe forming fabric 14. The vacuum box 18 applies a suction force to thewet web thereby removing moisture from the web.

From the forming fabric 14, the wet web 16 is transferred to a transferfabric 20. The transfer may be carried out using any suitable mechanism.As shown in FIG. 2, in this embodiment, the transfer of the web from theforming fabric 14 to the transfer fabric 20 is done with the assistanceof a vacuum shoe 22.

In one embodiment, the web 16 may be transferred from the forming fabric14 to the transfer fabric 20 while the transfer fabric 20 is travelingat a slower speed than the forming fabric 14. For example, the transferfabric may be moving at a speed that is at least 5%, at least 8%, or atleast 10% slower than the speed of the forming fabric. This process isknown as “rush transfer” and may be used in order to impart increasedmachine direction stretch into the web 16.

From the transfer fabric 20, the tissue web 16 is transferred to athroughdrying fabric 24 and carried around a cylindrical deck 26 of athrough-air dryer generally 28 made in accordance with the presentinvention. As shown, the through-air dryer 28 includes a hood 30. A hotgas, such as air, used to dry the tissue web 16 is created by a burner32. More particularly, a fan 34 forces hot air created by the burner 32into the hood 30. Hood 30 directs the hot air through the tissue web 16carried on the throughdrying fabric 24. The hot air is drawn through theweb and through the cylindrical deck 26.

At least a portion of the hot air is re-circulated back to the burner 32using the fan 34. In one embodiment, in order to avoid the build-up ofmoisture in the system, a portion of the spent heated air is vented,while a proportionate amount of fresh make-up air is fed to the burner32.

In the embodiment shown in FIG. 2, heated air travels from the hood 30through the drying cylinder 26. It should be understood, however, thatin other embodiments, the heated air may be fed through the dryingcylinder 26 and then forced into the hood 30.

While supported by the throughdrying fabric 24, the tissue web 16 isdried to a final consistency of, for instance, about 94% or greater bythe through-air dryer 28. The tissue web 16 is then transferred to asecond transfer fabric 36. From the second transfer fabric 36, the driedtissue web 16 may be further supported by an optional carrier fabric 38and transported to a reel 40. Once wound into a roll, the tissue web 16may then be sent to a converting process for being calendered, embossed,cut and/or packaged as desired.

In the system and process shown in FIG. 2, only a single through-airdryer 28 is shown. It should be understood, however, that the system mayinclude a plurality of through-air dryers if desired. For example, inone embodiment, a pair of through-air dryers may be arranged in series.One through-air dryer may be for partially drying the web while thesecond through-air dryer may be for completing the drying process.

Referring to FIGS. 3-6, more detailed views of the through-air dryer 28are shown. As shown particularly in FIGS. 3 and 5, the through-air dryer28 includes, in this embodiment, a stationary support shaft 50 that isconcentrically positioned with respect to the cylindrical deck 26. Theshaft 50 extends from a first side of the through-air dryer 28 to asecond and opposite side. The deck 26 is intended to rotate about theshaft 50. In this regard, a support structure exists in between theshaft 50 and the cylindrical deck 26.

The support structure includes a first hub 52 and a second hub 54. Thehubs 52 and 54 support each end of the cylindrical deck 26. As shown inFIG. 5, the hub 52 may be made from multiple pieces or components 56A,56B, 56C, and 56D. Each of the components 56A, 56B, 56C and 56D areconnected together and also are connected to the cylindrical deck.Further, the hub 52 includes passages for permitting air flow throughthe hub. For example, as shown in FIG. 5, the hub 52 can generally beconsidered to have a spoked arrangement.

Referring back to FIG. 3, in this embodiment, the through-air dryer 28further includes various other internal components that assist insupporting the cylindrical deck 26. For instance, the through-air dryer28 includes a rotating tube 58, a first internal support member 60, asecond internal support member 62, and a deck support ring 64, that allrotate with the cylindrical deck. As shown, the internal support members60 and 62 are attached to the rotating tube 58 on one end and to thedeck support ring 64 on an opposite end. In this manner, the decksupport ring supports the cylindrical deck 26 at a mid region betweeneach end of the cylindrical deck.

The internal support members 60 and 62 can be in the shape of platesand, as will be described in more detail below, can assist in directingair flow through the dryer. The internal support members 60 and 62 maybe of a single piece construction or may be of a multi-piececonstruction as desired.

Referring to FIGS. 3-5, the cylindrical deck 26 is shown in greaterdetail. As opposed to many conventional through-air dryers in which thecylindrical deck is made from a single piece of welded material, in thisembodiment, the cylindrical deck 26 comprises a plurality of individualplates 70. The plates are connected to the hubs 52 and 54 at each end.Specifically, the plates 70 may be connected to the hubs 52 and 54 in amanner that allows for thermal expansion. For example, as shown in FIG.3, the plates 70 may be connected to the hubs 52 and 54 using a pinconnection. For example, as can be seen in the embodiment illustrated inFIG. 3A, each plate 70 may be connected to hub 52 and hub 54 (not shownin FIG. 3A) using a pin connection that allows thermal expansion. Forinstance, plate 70, carrying throughdrying fabric 24 and web 16, mayinclude an indentation to allow thermal expansion while connected to hub52, as shown. Likewise, the plates 70 may also be connected to the decksupport ring 64 in a manner that allows thermal expansion. For instance,in one embodiment, each plate may include an indentation into which thedeck support ring 64 is received. In this manner, the plates 70 may moverelative to the deck support ring 64 while remaining supported by thedeck support ring.

In FIG. 4, the deck plates 70 are shown supporting a throughdryingfabric 24 which is used to carry a web 16 being dried. In the embodimentshown in FIG. 4, hot gases flow through the web 16, through thethroughdrying fabric 24, and in between the deck plates 70. The deckplates 70 should be spaced apart a distance sufficient to permit gasflow through the plates while also being spaced a distance sufficient tosupport the throughdrying fabric 24.

The actual distance that the deck plates 70 are spaced apart depends onvarious factors, including the size of the through-air dryer 28, theamount of load being placed upon the through-air dryer and the amount ofgas flow through the dryer. In general, the deck plates 70 may be spacedfrom about 12 millimeters (1/2 inches) to about 254 millimeters (10inches) apart, such as from about 1 inch to about 6 inches apart. Forexample, when the cylindrical deck 26 has a diameter of about 5 meters(16.4 feet) the plates 70 may be spaced apart 75 millimeters (2.95inches).

In order to facilitate air flow through the cylindrical deck 26, asshown in FIG. 4, the deck plates 70 may be tapered. In particular, thedeck plates are tapered in a direction opposite gas flow. In thismanner, the gas flow is more easily initially passed through thecylindrical deck and then accelerated as the gases pass the deck plates70.

In order to prevent wear of the throughdrying fabric 24, the deck plates70 may be coated with a material that reduces the coefficient offriction. For example, in one embodiment, the deck plates may be coatedwith a polytetrafluoroethylene coating marketed as Teflon® by the DupontCompany or a low wear ceramic coating as manufactured by PraxairCoatings.

As described above, the cylindrical deck 26 and all of the componentsthat support the deck rotate about the stationary axis 50. In order topermit rotation of the deck, each of the hubs 52 and 54 are inassociation with a respective bearing 72 and 74. Of particularadvantage, the bearings are positioned so as to be in substantialalignment with each end of the cylindrical deck 26. In this manner, nosignificant moment transfers occur between the deck and the supportstructure as diagrammatically shown, for instance, in FIG. 6. Asillustrated in FIG. 6, the through-air dryer 28 is shown supporting aload 6 without the creation of the moments shown in FIG. 1.

In past through-air dryer configurations, as shown in FIG. 1, bearingswere placed outside of the cylindrical deck in order to prevent thebearings from being contacted with the hot gas flow circulating throughthe dryer. In the through-air dryer illustrated in FIG. 3, however, thebearings 72 and 74 are shielded from air flow by the rotating tube 58which is connected on one end to the hub 52 and on the opposite end tothe hub 54. Thus, the bearings 72 and 74 are protected from high levelsof heat transfer from the hot, humid air inside the through-air dryer.

As described above, gas flow direction through the through-air dryer 28may be either from the hood 30 through the cylindrical deck 26 orthrough the cylindrical deck 26 and into the hood 30. When gas flowenters the through-air dryer through the cylindrical deck 26, the webbeing dried may be placed on top of the throughdrying fabric 24 as shownin FIG. 4. In this embodiment, gas flows through the web 16, through thethroughdrying fabric 24 and between the deck plates 70. From the deckplates 70, the gas contacts the internal deck supports 60 and 62 asshown in FIG. 3. The internal deck supports 60 and 62 redirect the gasout through the hubs 52 and 54. Not shown, the hubs 52 and 54 may beplaced in communication with a conduit for receiving the gas exiting thedryer. Once exiting the hubs 52 and 54, the gas may be collected andrecycled as desired.

As shown in FIG. 2, the throughdrying fabric 24 is wrapped partiallyaround the cylindrical deck 26 of the through-air dryer 28 leaving anopen end towards the bottom of the deck. In the past, due to theconstruction of the through-air dryers, internal baffles were typicallyplaced inside the cylindrical deck to prevent ambient air from enteringthe dryer.

One further advantage to the through-air dryer of the present inventionis that the configuration of the through-air dryer does not require thatthe baffles be placed inside the cylindrical deck 26. Instead, as shownin FIG. 2, an external baffle generally 80 may be placed adjacent to thecylindrical deck over the open free end. As shown in FIG. 2, theexternal baffle 80 extends from one side of the throughdrying fabric 24to an opposite side of the throughdrying fabric in order to preventambient air from entering the through-air dryer.

Another advantage to the through-air dryer of the present invention isthat the dryer includes many multi-piece components. For example, thecylindrical deck is made from a plurality of deck plates 70. Also, mostof the internal support members may be made from multiple parts.

Due to the construction of the through-air dryer 28, the through-airdryer may be manufactured and shipped having a shipping volume that ismuch less than the assembled volume of the dryer. For instance, in oneembodiment, the largest dimension of the shipping volume is no greaterthan one half the diameter of the cylindrical deck. In this manner,expenses involved in shipping the through-air dryer are drasticallyreduced in comparison to many conventional dryers. In many locations inthe world it is not physically possible or very difficult to ship afully assembled dryer because of the limits of height, width and weightimposed for normal roadways or railroads.

Still another advantage to the through-air dryer of the presentinvention is the ability to easily calculate loads that are placed onthe dryer during operation. The loads are easily calculated since thereis no transfer of moment between the deck and support structure of thethrough-air dryer and since the deck is made of simple plates ratherthan a complicated welded structure. Typical decks are welded from amultitude of formed sheet metal components that are too complex toanalyze using traditional analytical methods. Finite element analysis(FEA) can be used, but the complexity of the deck is generally beyondcomputing power except for small sections. To calculate the loads on awelded dryer deck, the properties of a small section are calculated indetail and the results are used as an average to compute the stresses onthe entire deck. The stresses on the deck and the stresses caused bythermal expansion must then be used to compute the moment created acrossthe interface between the deck and support structure. A completeexplanation of calculating loads for one embodiment of a through-airdryer made in accordance with the present invention is included in theexamples below.

EXAMPLE 1

One feature of the through-air dryer (“TAD”) design of the presentinvention is the ability to rapidly calculate loads and deflectionsanalytically using well-established mechanical engineering principles.The purpose of this example is to show analytical methods that may beused to calculate the deflections and loads on support bars for a TADmanufactured using the principles of this invention.

The TAD dryer deck is formed from a multiplicity of individual platesdefining a cylinder. Each deck plate comprises a simply supportedsection bar as shown in FIG. 7.

The bar has an axial length (l), a radial width (w) and a thickness (t).For the purposes of this example the thickness and width is fixed asconstant. Designs can be adjusted to vary both thickness and width tooptimize the use of materials and enhance the process. For example thewidth can be varied to be larger at the locations of highest stress,generally in the center of an unsupported span. Likewise the thicknesscan be varied to be thin at the interface with the fabric to minimizewet spots, but be thick away from the fabric to add rigidity.

As shown in FIG. 7, there is a distributed unit load on the bar composedof the weight of the bar itself, fabric tension, pressure differentialand centripetal acceleration of the bar on the rotating surface of theTAD deck. Each one of these loads will be calculated separately andsummed to determine the total distributed load on the bar. Note that theload is not the same depending on the location of the bar. For example,areas of the dryer that are wrapped with the fabric subject the bar tothe resultant of fabric load while areas of no fabric wrap have no loadassociated with the fabric.

Weight

The weight of the bar per unit length is calculated from the volumemultiplied by the density of the material for one unit length. This canbe calculated as:ω=w·t·l·δ   Eq. 1where: w=weight per unit length

-   -   w=width    -   t=thickness    -   l=unit length    -   δ=density of material        Fabric Tension

The calculation of fabric tension requires additional information aboutthe relative geometry between bar elements. The fabric tension is theresultant force of tension pulling on the bar because of the change ofdirection of the fabric across the bar.

FIG. 8 shows a schematic of fabric tension acting on headbox bars.Fabric tension (T) creates a force on the bar by the change in angle ofthe fabric over the bar. The angle (θ) is determined by the 360° dividedby the number of bars. A further example of a specific case will showthe effect of changing the number bars versus the size of each bar toreduce the amount of deflection of the bar in service. A free bodydiagram of the bar shows that the resultant force on the bar (F_(t)) isas follows: $\begin{matrix}{F_{t} = {{2 \cdot T \cdot \sin}\quad\left( \frac{\theta}{2} \right)}} & {{Eq}.\quad 2} \\{{{Where}\text{:}{~~~}F_{t}} = {{Force}\quad{per}\quad{unit}\quad{length}\quad{from}\quad{tension}}} & \quad \\{\quad{T = {{Fabric}\quad{tension}\quad{per}\quad{unit}\quad{length}}}} & \quad \\{\quad{\theta = {{Change}\quad{in}\quad{angle}\quad{between}\quad{bars}}}} & \quad\end{matrix}$Pressure

Gas or air flow is a process parameter that helps to determine thedrying capacity of the TAD. Air flow creates differential pressureacross the deck of the TAD and creates a load on the bars which comprisethe deck. Referring further to FIG. 8 the distance (d₁) and the length(l) of the bar defines the chordal area where the pressure is appliedthat needs to be supported by each bar. Even though the pressure isapplied to an angled surface, the principle of projected area allows theuse of the chordal distance as the pressure area.

It can be seen by rotational symmetry that the distance (d₁) isequivalent to distance (d₂) which is the chordal distance betweenadjacent bars. Using this definition and using (d) as the distancebetween the bars the distance (d) can be calculated as: $\begin{matrix}{d_{1} = {d_{2} = {d = {{2 \cdot r_{0} \cdot \sin}\quad\left( \frac{\theta}{2} \right)}}}} & {{Eq}.\quad 3} \\{{{Where}\text{:}{~~~}d} = {{Chordal}\quad{distance}\quad{between}\quad{bars}}} & \quad \\{\quad{r_{o} = {{Outside}\quad{radius}\quad{of}\quad{TAD}}}} & \quad \\{\quad{\theta = {{Change}\quad{in}\quad{angle}\quad{between}\quad{bars}}}} & \quad\end{matrix}$

The pressure is applied over an area defined by the length (l) and thedistance (d). The force (F_(p)) generated for each bar can then bedefined as:F _(p) =ΔP·d·l   Eq. 4Where: F_(p)=Force from differential pressure

-   -   d=Distance as defined in FIG. 8    -   l=Unit length of bar

Substituting the value for distance (d) yields the following equationfor the force created by differential pressure: $\begin{matrix}{F_{p} = {{2 \cdot \Delta}\quad{P \cdot r_{0} \cdot l \cdot \sin}\quad\left( \frac{\theta}{2} \right)}} & {{Eq}.\quad 5} \\{{Where}\quad{the}\quad{variables}\quad{are}\quad{defined}\quad a\quad{{bove}.}} & \quad\end{matrix}$Rotational Force

The rotation of the TAD causes forces to be applied to the bar.Specifically the bar tends to be thrown outward because of its locationon the periphery of the TAD. The centripetal acceleration of the bar canbe calculated using well-known mechanical principles. The force on thebar is a product of its mass and the acceleration of the bar caused bythe constant change of direction of the bar. Centripetal acceleration isdefined as the acceleration towards the center of the roll or in thenormal direction relative to travel.

As a general case, it is possible to estimate the force created by a barby using the centroid of the bar as the radius and the tangentialvelocity of the centroid as the velocity. This is the averagecentripetal acceleration of the bar. Since this design can be applied tosmall rolls, such as transfer rolls, as well as TADs and since the widthof the bar can be a significant portion of the outside radius of theroll, a better method is to develop a general formula what includes thewidth of the bar. It can be seen that portions of the bar closer to thecenter of the roll have a lower velocity and a smaller radius. Since thevelocity is squared, portions of the bar closer to the center of theroll contribute less to the force than portions nearer the periphery.

The normal acceleration is: $\begin{matrix}{a_{n} = \frac{v^{2}}{r}} & {{Eq}.\quad 6} \\{{{Where}\text{:}\quad a_{n}} = {{Centripetal}\quad{acceleration}}} & \quad \\{\quad{v = {{Tangential}\quad{velocity}}}} & \quad \\{\quad{r = {{Radius}\quad{of}\quad{curvature}}}} & \quad\end{matrix}$

Therefore the force on the bar from rotation of the dryer can becalculated based on Newton's third law as:F _(n) =m·a _(n)   Eq. 7Where: F_(n)=Normal force on bar from rotation

-   -   m=Unit mass of bar    -   a_(n)=Centripetal acceleration        or with substitution is: $\begin{matrix}        {{F_{n} = {m \cdot \frac{v^{2}}{r}}}\quad} & {{Eq}.\quad 8} \\        {{Where}\quad{variables}\quad{are}\quad{defined}\quad a\quad{{bove}.}} & \quad        \end{matrix}$

Using the centroid of the bar as shown in FIG. 9 an estimate for theforce caused by rotation can be determined by substituting the radius ofthe centroid and the velocity of the centroid for v and r in theequation above. $\begin{matrix}{r_{c} = {{\frac{r_{o} + r_{i}}{2}\quad{and}\quad v_{c}} = {v_{o}\left( \frac{r_{o} + r_{i}}{2 \cdot r_{o}} \right)}}} \\{{{Where}\text{:}\quad r_{c}} = {{radius}\quad{of}\quad{centroid}\quad{of}\quad{support}\quad{plate}}} \\{\quad{v_{c} = {{tangential}\quad{velocity}\quad{of}\quad{centroid}}}}\end{matrix}$Then an estimate for the normal force on the bar from rotation can bedetermined as follows: $\begin{matrix}\begin{matrix}{F_{n} = {m \cdot \frac{v_{o}^{2}\left( {r_{o} + r_{i}} \right)}{2 \cdot r_{o}^{2}}}} \\{{Where}\quad{the}\quad{variables}\quad{are}\quad{defined}\quad a\quad{{bove}.}}\end{matrix} & {{Eq}.\quad 9}\end{matrix}$Or substituting for m the equation becomes: $\begin{matrix}\begin{matrix}{F_{n} = {w \cdot l \cdot t \cdot \delta \cdot \frac{v_{o}^{2}\left( {r_{o} + r_{i}} \right)}{2 \cdot r_{o}^{2}}}} \\{{Where}\quad{the}\quad{variables}\quad{are}\quad{defined}\quad a\quad{{bove}.}}\end{matrix} & {{Eq}.\quad 10}\end{matrix}$

A more accurate value of the force (F_(n)) can be calculated byintegrating the unit force along the length of the bar along the widthfrom the inside of the bar to the periphery. In FIG. 9 a bar is shownrelative to the center of the TAD. The inner radius (r_(i)) correspondsto the swept surface on the interior of the bars and outer radius(r_(o)) corresponds to the outside surface of the TAD swept by thesupport bars. Length (l) of the bar is the axial dimension across thesurface of the TAD and thickness (t) in the circumferential direction.Note that the width (w) of the bar is determined by the differencebetween the inner and outer radii.

Velocity of the TAD is usually expressed in the velocity of the surfacewhich is designated as the outer velocity (V_(o)) in FIG. 9. Based onthe dimensions of the bar and the distance from the center of the TADanother velocity of the inner surface can be defined as the innervelocity (V_(i)) a value that is always less than the outer velocity andproportional to the outer velocity in the ratio of the inner to outerradii. A reference radius (r) is also defined which is a point betweenthe inner and outer radius along the width of the support bar. Aninfinitesimal section of the bar at radius (r) is defined as “dr.” Withthese definitions it is possible to see that the force of section “dr”is defined as:dF _(n) =dm·a _(n)   Eq. 11Where: dF_(n)=Normal force on bar section from rotation

-   -   dm=Unit mass of bar    -   a_(n)=Centripetal acceleration        Also note that a section of bar is composed of an element of        mass as follows:        dm=l·t·δ·dr   Eq. 12        Where: dm=Unit mass of bar    -   t=thickness    -   l=unit length    -   δ=density of material    -   dr=section of support bar        Also note that the velocity of the bar at distance “r” from the        center of the TAD roll is defined as: $\begin{matrix}        {{V(r)} = {V_{i}\frac{r}{r_{i}}}} & {{Eq}.\quad 13} \\        {{{Where}\text{:}\quad{V(r)}} = {{Velocity}\quad{at}\quad{distance}\quad{``r"}}} & \quad \\        {\quad{V_{i} = {{Velocity}\quad{at}\quad{``r_{i}"}}}} & \quad \\        {\quad{r_{i} = {{radius}\quad{on}\quad{inside}\quad{of}\quad{support}\quad{bar}}}} & \quad \\        {\quad{r = {{distance}\quad{from}\quad{center}\quad{of}\quad{TAD}}}} & \quad        \end{matrix}$        Using this value it can be seen that the centripetal        acceleration is now: $\begin{matrix}        {a_{n} = {{\left( {V_{i}\frac{r}{r_{i}}} \right)^{2}\left( \frac{1}{r} \right)} = {\frac{V_{i}^{2}}{r_{i}^{2}}r}}} & {{Eq}.\quad 14} \\        {{Where}\quad{the}\quad{variables}\quad{are}\quad{defined}\quad a\quad{{bove}.}} & \quad        \end{matrix}$        The centripetal acceleration is seen to vary directly with the        radius at constant surface speed. Therefore substituting the        centripetal acceleration and dm into the equation for dF_(n),        and integrating from r_(i) to r_(o) gives the following result        for F_(n). $\begin{matrix}        {{{dF}_{n} = {{l \cdot t \cdot \delta \cdot \frac{V_{i}^{2}}{r_{i}^{2}}}{r \cdot {dr}}}}{{{therefore}:F_{n}} = {{l \cdot t \cdot \delta \cdot \frac{V_{i}^{2}}{r_{i}^{2}}}{\int_{r_{i}}^{r_{o}}{r \cdot {dr}}}}}} & {{Eq}.\quad 15}        \end{matrix}$        Integrating and substituting the values r_(i) and r_(o) yields        the following equation for F_(n). Note that the constant is zero        because the F_(n) at zero is zero. $\begin{matrix}        {{F_{n} = {{l \cdot t \cdot \delta \cdot \frac{V_{i}^{2}}{2 \cdot r_{i}^{2}}}\left( {r_{o}^{2} - r_{i}^{2}} \right)}}{Where}\quad{the}\quad{variables}\quad{are}\quad{defined}\quad{{above}.}} & {{Eq}.\quad 16}        \end{matrix}$        This equation is the more general form used to calculate the        force created on the support bars from TAD rotation.        Deflection

The amount of deflection of the bar under load is a consideration fortissue machine design since deflection can have an adverse effect on theability of the fabric to guide or can cause the fabric to developwrinkles which make it unusable. The total load on each support bar isthe sum of the weight of the bar, force from fabric tension, force fromdifferential pressure and rotational forces. The combination of theseforces causes deflection of the bar with the maximum deflectiontypically near the center of the unsupported span. Note that the load isnot constant around the circumference of the TAD since the fabric doesnot wrap the entire TAD surface. That is, fabric tension forces anddifferential pressure forces only exist in areas that are wrapped by theTAD fabric. Also, the direction of the force changes with the positionof the bar during the rotation of the TAD. For example, the weight ofthe bar is always directed downwards, rotational forces are directedradially outwards, and fabric tension and differential pressure forcesare directed radially inwards towards the center of the TAD. The changesin direction of forces are shown schematically in FIG. 10.

Referring to FIG. 10, “T” represent the fabric tension, “P” force fromdifferential pressure, “w” force from weight, and “a” force fromcentripetal acceleration. At the 12 o'clock position on the TAD it canbe seen that the centripetal acceleration tends to reduce the overallforce while at the 6 o'clock position it add to the force from theweight of the bar.

It is necessary to calculate the load at key positions on the TAD deckto ensure that all potential cases are accounted for. It is alsopossible to calculate the fluctuation in load at a given speed which isimportant for the design of the end connections and to analyze potentialreduction in life from fatigue loading.

Deflection is a function of the type of loading, type of endconnections, load applied and the properties and geometry of thematerial used. For the case of the support bars, by definition of theinvention, no moment is transferred between the support bars and thehead so the bars are simply supported. This means that there is a singlereaction force at each end of the bar designated as “R” in FIG. 7. Allloads on the bar are distributed loads, that is, they do not act at apoint, but have a uniform nature over a defined distance. All loads forthe case of the support bar act over the entire length of the bar. Usingaccepted principles in mechanics it is possible to sum the loads todetermine a combined final distributed load on the bar.

For small amounts of deflection, as present in the TAD support bars, itis acceptable to use standard beam deflection equations. The specificequation for a simply support beam with a distributed load is asfollows: $\begin{matrix}{{f = {\frac{W}{EI}\frac{5 \cdot l^{3}}{384}}}{{{Where}:f} = {deflection}}{{W = {{Total}\quad{load}}},{{that}\quad{is}\quad w \times l}}{{E = {{Young}^{\prime}s\quad{Modulus}\quad{of}\quad{material}}}I = {{Rectangular}\quad{moment}\quad{of}\quad{inertia}}}{l = {{length}\quad{of}\quad{bar}}}} & {{Eq}.\quad 17}\end{matrix}$Note that for a simply supported beam the deflection is five times ashigh as the deflection of a fully supported beam. The equation fordeflection can be rearranged noting that W=wl as follows. Note that foran equivalent unit load the deflection varies with the fourth power oflength showing that the addition of internal supports to the bar is verybeneficial to reducing deflection. $\begin{matrix}{{f = {{\frac{w}{EI}\frac{5 \cdot l^{4}}{384}\quad{{Where}:w}} = {{unit}\quad{load}}}}\text{}\quad{{Other}\quad{variables}\quad{defined}\quad{{above}.}}} & {{Eq}.\quad 18}\end{matrix}$

It can be seen that standard mechanical engineering techniques permit ananalytical solution to the calculation of loads and deflection of thesupport bars for a TAD deck. The key is to have the bars simplysupported so the moment is not transmitted to the heads of the TAD.

EXAMPLE 2

The following is a prophetic example using the equations derived inExample 1. Typical dimensions of a through-air dryer (“TAD”) were used.A typical TAD for the manufacture of tissue paper products is about 5 m(16.4 feet) in diameter, has a width of 5.2 m (17.1 feet). A typicalmaximum operating speed is 1500 m/min (4921 ft/min) at the surface ofthe deck. Maximum deflection of 3 millimeters (⅛ inch) is allowedalthough less is preferable to prevent premature wear or wrinkling ofthe fabric. For the case of this example, the bars are rectangular inshape although there are advantages to reducing the thickness of the barat the periphery of the TAD where the bars contact the fabric to preventnon-uniform air flow as previously discussed.

Also, a rectangular bar is not the optimum shape for maximizing therectangular moment of inertia relative to the weight. A manufacturedmaterial consisting of a tube with wearing surfaces would provide morerigidity especially to prevent buckling failure in unsupported areas.These types of shapes are readily available and can be readilycalculated using the principles discussed in this example.

The spacing of the bars needs to adequately support the fabric andspread the load from differential pressure and fabric tension. Areasonable spacing is 75 millimeters (2.95 inches), but larger spacingcan be accommodated if an intermediate support structure is insertedbetween the support bars to support the fabric and prevent oscillationsin fabric tension from the chordal distances between the support bars.Note that the main support remains the axially oriented bars. Theselection of the number of bars is generally the maximum possible tominimize overall weight, commensurate shipping costs and handling, andto reduce assembly time at the site of use. Based on a spacing of 75millimeters and a dryer diameter of 5 meters with a circumference of15,707 millimeters, the number of bars will be 210, rounded to thenearest whole number. Based on the number of bars, it is possible tocalculate that the change in angle between each bar will be 1.71degrees. This angle is used to determine the forces from tension anddifferential pressure.

The support bar dimensions ultimately determine the amount of deflectionand contribute to the overall weight of the TAD. Another factordetermined by bar dimensions is the number of internal supports thatwill be required to minimize deflection. Deflection varies with thefourth power of length so a support in the center of the dryer willreduce deflection by a factor of sixteen. Additional supports will berequired to prevent buckling failure from twisting, or movement in thecircumferential direction as a simple bar has little stiffness in thisdirection. It was determined that a suitable bar dimension for thisexample is a bar with dimensions of 180 millimeters (7.4 inches) in theradial dimension (width) and 7 millimeters (0.28 inches) in thicknessfor a bar that is solid and rectangular in cross section.

The thickness of the bar and the number of bars determine the amount ofopen area of the dryer which is calculated as a percentage of therotated surface of the dryer that is not blocked by bars relative to theentire surface. For this example the open area is calculated to be 91%which is calculated as the ratio of the area of the outside surface ofthe through-air dryer less the area of the thickness of the bar to thesurface of the through-air dryer. Note that it is advantageous to taperthe tip of the support bar to retain the stiffness while increasing theopen area of the dryer. It is expected that a final bar design will beoptimized to increase open area, minimize stiffness and maximizestiffness in the radial and circumferential directions. A structure suchas a hollow could be used to reduce weight while increasing stiffness.

The dimensions of the bar give the weight per unit load based onEquation 1. The material of construction is mild steel. The density ofsteel is 7756 kg/m² (0.28 lb/in²) so the load contributed by the bar canbe calculated to be 0.10 kN/m (0.57 lb/in). Note that the loadcontributed by weight is always directed downwards and is present in alllocations.

Fabric tension is typically in the range of 1.75 to 10.5 kN/m (10 to 60lb/in) for all fabrics. TAD fabrics are generally run at a maximum ofabout 4.4 kN/m (25 lb/in). Therefore this example uses 4.4 kN/m (25lb/in) as the fabric tension.

The force of the fabric is the resultant force on the bar from fabrictension as determined by Equation 5. The angle is the change in anglebetween adjacent bars as shown in FIG. 8. For this example the angle θis 1.71 degrees so the resultant force from tension is therefore 0.13kN/m (0.74 lb/in). It can be seen that closer spacing from having moresupport bars in the design will reduce this value. Note that fabrictension only creates a force when the fabric is present, which for thisexample is about 260 degrees of wrap. When fabric tension is present italways creates a force that is directed radially towards the centerlineof the TAD cylinder.

Rotational forces are created by a combination of the mass of the barand the continual acceleration of the bar towards the center of the TADto maintain its circular path. In general, it is preferable to useEquation 15 to calculate the force from rotational load, although forexamples where the radial dimension of the bar is much smaller than theradius of the dryer the results using Equation 10. Based on a speed of1500 meters/minute (4921 feet/minute) or 25 meters/second, an outerradius of 2.5 meters and a bar dimension of 170 millimeters by 7millimeters, the force from rotation is 2.36 kN/m. Rotational force isalways directed away from the center of the TAD and is always presentwhen the dryer is rotating. The force from rotation is proportional tothe square of speed so that load increases parabolically with speed. Forthis example the load from rotational forces has the highest magnitudeof the four forces considered.

Each of the four forces, which are load from weight, fabric tension,differential pressure and rotation create a uniform distributed load onthe bar. A feature of beam loading of any type is that it is possible tosum the effect of each component of load to determine the overall load,commonly referred to as the principle of superposition. For the case ofthe support bar the overall load is a sum of each of the four loadspreviously mentioned based on the current location of the bar relativeto gravity and the fabric loading. As previously mentioned, fabrictension and differential pressure are only present in parts of thecircumference of the dryer that are in contact with the fabric. Notethat differential pressure is not required to be present for the entirecontact surface of the fabric, but this is beneficial and common tomaximize the drying capability of the TAD.

Since deflection of the bar relative to the center of the TAD isimportant for structural reasons, load will be considered in thepositive direction away from the center of the TAD and negative towardsthe center of the TAD. This leads to positive and negative deflection inthe same sense as the load. The sum of the loads in the instantaneousposition of the bar relative to gravity and the presence or absence ofthe fabric determine the final load. To help to illustrate this a tableof loads has been developed below. It can be seen that the significantload on the dryer is actually away from the center of the dryer at anoperating speed of 1500 meters per minute and that the maximum loadoccurs at the 6 o'clock position where there is no counteracting forcefrom fabric tension and differential pressure but weight and rotationalforces are additive. Radial Force (kN) at Different Positions LoadSource 12 o'clock 3 o'clock 6 o'clock 9 o'clock Weight 0.10 0.00* −0.100.00* Fabric Tension 0.13 0.13 0.00 0.13 Differential 0.56 0.56 0.000.56 Pressure Rotation −2.36 −2.36 −2.36 −2.36 Total −1.57 −1.67 −2.46−1.67*force from weight not radial in direction.Also to note is that the weight does not contribute to radial forces inthe 3 o'clock and 9 o'clock positions since weight always creates adownward force.

Deflection of the bar is calculated using Equation 18. These equationsare developed from four successive integrations of the load on a beamand are accurate for small deflections relative to the length of thebeam. Equation 18 is for a simply supported beam which means that thebeam is supported at each extremity, but no moment is transferred fromthe beam to the supports. The deflection of the bar calculates to be0.837 inches at the 12 o'clock position and 1.307 inches at the 6o'clock position.

Using a center support changes the load case from a simply supportedbeam to a beam that is simply supported on one end and cantilevered onthe other. A free body diagram of half the bar shows the moment which issymmetrical for each side. Note that the moments now present at thecenter support are internal to the bar and are not transferred to otherTAD components.

The equation for deflection of a beam with a distributed load, simplysupported on one end and cantilevered on the other end is as shown inEquation 19 below. There is a reduction of one sixteenth because of thefourth power change from reducing the span by half and an additional 2.4times reduction from cantilevering the beam at one end for a totalreduction in deflection of 38.5 times by installing a support in thecenter span. The deflection is now reduced to 0.022 inches at the 12o'clock position and 0.034 inches at the 6 o'clock position.$\begin{matrix}{{f = {{\frac{w}{EI}\frac{l^{4}}{185}\quad{{Where}:w}} = {{unit}\quad{load}}}}\text{}\quad{{Other}\quad{variables}\quad{defined}\quad{{above}.}}} & {{Eq}.\quad 19}\end{matrix}$

The maximum stress in the beam occurs in the extreme edges of the widthscommonly referred to as the “outer fibers” when discussing stress inbeam theory. The maximum stress occurs at a location of maximum momentin the beam, such as at mid-span for a simply supported beam, and at theoutermost fiber of the beam. It can be calculated by using the followingEquation 20 below: $\begin{matrix}{{\sigma_{\max} = {\frac{M\quad c}{I}\quad{Where}}}\text{}{M = {{the}\quad{maximum}\quad{moment}}}{c = {{distance}\quad{from}\quad{the}\quad{neutral}\quad{axis}}}{I = {{rectangular}\quad{moment}\quad{of}\quad{inertia}}}} & {{Eq}.\quad 20}\end{matrix}$

The distance “c” is the maximum distance from the neutral axis of thecross section of the beam. A simple bar has the neutral axis at thecenter line of the beam or at 85 millimeters from the edge. Therefore“c” is the same distance of 85 millimeters from the neutral axis to theouter fiber. The maximum moment is calculated from the beam equationsas: $M_{\max} = {\frac{{wl}^{2}}{8}\quad{at}\quad\frac{3l}{8}}$for simply support beam, distributed load$M_{\max} = {\frac{9}{128}{wl}^{2}\quad{at}\quad\frac{3l}{8}}$from the simply supported end for a simply/cantilevered beam

The maximum moment for the simply supported case with full span can becalculated as 8.28 kNm and as 1.17 kNm for the case with a centersupport. Note the center support reduces the length “l” in half and alsothe different load case provides a further reduction in moment.Therefore using Equation 20 it can be seen that the maximum level ofstress is 31,412 lb/in² for the simply supported case and 4,417 lb/in²for the case with a support. The range of load at operating speed isseen to be varying, but always in the same sense, that is, there is noreversal of stress which greatly reduces the impact of fatigue loadingon the bars.

The load on the bar that is not directed radially is also important tonote. This occurs with the force from the weight of the bar in the 3o'clock and 9 o'clock positions. While the load is small, the areamoment of inertia of the bar is 660 times lower that the area moment ofinertia in the radial direction. Supporting the bars between each otherfor this design in three locations evenly spaced across the length ofthe bar will reduce the deflection. Supports do not have to be connectedto the center axis of the TAD, but may be between the individual barsthemselves.

It is also advantageous to provide additional calculations to test thatvibration will not be a concern and to test any stress concentrationsthat arise from machining of the bar from its standard rectangularprofile. This would include, but is not limited to, holes required formounting the center support and stiffening components and the connectionof the bar to the deck.

These and other modifications and variations to the present inventionmay be practiced by those of ordinary skill in the art, withoutdeparting from the spirit and scope of the present invention, which ismore particularly set forth in the appended claims. In addition, itshould be understood that aspects of the various embodiments may beinterchanged both in whole or in part. Furthermore, those of ordinaryskill in the art will appreciate that the foregoing description is byway of example only, and is not intended to limit the invention sofurther described in such appended claims.

1-18. (canceled)
 19. An apparatus for through-air drying webscomprising: a rotatable cylindrical deck having sufficient open space topermit air flow therethrough, the rotatable cylindrical deck comprisinga plurality of individual deck plates; a support structure positioned tosupport the rotatable cylindrical deck, the support structure beingattached to the individual deck plates; and a support shaftconcentrically positioned with respect to the rotatable cylindricaldeck, the support structure being mounted on the support shaft.
 20. Anapparatus as defined in claim 19, wherein the individual deck plates areattached to the support structure using a pin attachment structure. 21.An apparatus as defined in claim 19, wherein the deck plates have across sectional profile that tapers in a direction opposite thedirection of gas flow through the cylindrical deck.
 22. An apparatus asdefined in claim 19, wherein the support structure is configured torotate on the support shaft and wherein the apparatus further comprisesat least one bearing positioned between the support shaft and thesupport structure to permit rotation of the support structure, thebearing being located so that there is substantially no moment transferbetween the cylindrical deck and the support structure.
 23. An apparatusas defined in claim 19, further comprising a hood surrounding thecylindrical deck for directing a hot gaseous stream through thecylindrical deck or away from the cylindrical deck.
 24. An apparatus asdefined in claim 19, further comprising a throughdrying fabric wrappedaround the cylindrical deck, the throughdrying fabric being configuredto carry a web over a portion of the surface of the deck.
 25. Anapparatus as defined in claim 24, wherein the throughdrying fabric iswrapped around the cylindrical deck from an upstream point to adownstream point leaving an open free end, and wherein the apparatusfurther comprises an external baffle positioned over the open free endof the cylindrical deck, the external baffle shielding the open free endof the drying cylinder from external air.
 26. An apparatus as defined inclaim 22, wherein the support structure comprises a first hub spacedfrom a second hub, each hub engaging an opposite end of the cylindricaldeck, the apparatus including a first bearing and a second bearing, thefirst bearing being positioned between the first hub and the supportshaft and the second bearing being positioned between the second hub andthe support shaft, each bearing being substantially in alignment witheach end of the cylindrical deck.
 27. An apparatus as defined in claim26, wherein the support structure further comprises: a rotating tubesurrounding the support shaft, the rotating tube being connected at afirst end to the first hub and at a second end to the second hub; atleast one internal deck support extending between the rotating tube andthe cylindrical deck; and a deck support ring supporting the cylindricaldeck in between the first end of the cylindrical deck and the second endof the cylindrical deck, the support ring being connected to the atleast one internal deck support.
 28. An apparatus as defined in claim27, wherein the support structure includes a first internal deck supportand a second internal deck support extending between the rotating tubeand the cylindrical deck, each of the deck supports being connected tothe deck support ring.
 29. An apparatus as defined in claim 19, whereinat least 80% of the surface of the cylindrical deck is open for allowinggas flow.
 30. An apparatus as defined in claim 28, wherein the firstdeck support and the second deck support have a useful shape fordirecting gas flow between the cylindrical deck and the first and secondhubs and wherein the rotating tube shields the first bearing and thesecond bearing from the gas flow.
 31. An apparatus for through-airdrying webs comprising: a cylindrical deck having sufficient open spaceto permit air flow therethrough; a stationary support shaftconcentrically positioned with respect to the cylindrical deck; and asupport structure positioned between the cylindrical deck and thesupport shaft for supporting the cylindrical deck, the support structurebeing configured to rotate on the support shaft, the support structurecomprising a first hub spaced from a second hub, each hub engaging anopposite end of the cylindrical deck, the support structure furthercomprising a rotating tube surrounding the support shaft, the rotatingtube being connected at a first end to the first hub and at a second endto the second hub.
 32. An apparatus as defined in claim 31, wherein thesupport structure further comprises at least one internal deck supportextending between the rotating tube and the cylindrical deck, and a decksupport ring supporting the cylindrical deck in between the first end ofthe cylindrical deck and the second end of the cylindrical deck, thesupport ring being connected to the at least one internal deck support.33. An apparatus as defined in claim 32, wherein the support structureincludes a first internal deck support and a second internal decksupport extending between the rotating tube and the cylindrical deck,each of the deck supports being connected to the deck support ring. 34.An apparatus as defined in claim 31, wherein the apparatus furthercomprises a first bearing and a second bearing, the first bearing beingpositioned between the first hub and the support shaft and the secondbearing being positioned between the second hub and the support shaft,each bearing being substantially in alignment with each end of thecylindrical deck.
 35. An apparatus as defined in claim 34, wherein thefirst and second bearings are located so that there is substantially nomoment transfer between the cylindrical deck and the support structure.36. An apparatus as defined in claim 31, further comprising a hoodsurrounding the cylindrical deck for directing a hot gaseous streamthrough the cylindrical deck or away from the cylindrical deck.
 37. Anapparatus as defined in claim 31, further comprising a throughdryingfabric wrapped around the cylindrical deck, the throughdrying fabricbeing configured to carry a web over a portion of the surface of thedeck.
 38. An apparatus as defined in claim 37, wherein the throughdryingfabric is wrapped around the cylindrical deck from an upstream point toa downstream point leaving an open free end, and wherein the apparatusfurther comprises an external baffle positioned over the open free endof the cylindrical deck, the external baffle shielding the open free endof the drying cylinder from external air.
 39. An apparatus as defined inclaim 31, wherein the cylindrical deck comprises a plurality ofindividual deck plates that are attached to the support structure. 40.An apparatus as defined in claim 39, wherein the individual deck platesare attached to the support structure using a pin attachment structure.41. An apparatus as defined in claim 39, wherein the deck plates have across sectional profile that tapers in a direction opposite thedirection of gas flow through the cylindrical deck.
 42. An apparatus asdefined in claim 39, wherein a load supported by the deck plates of thecylindrical deck is the sum of the following forces:ω = w ⋅ t ⋅ l ⋅ δ  where : ω = weight  per  unit  length  of  a  deck  platew = width t = thickness l = unit  length δ = density  of  material$F_{p} = {{{2 \cdot \Delta}\quad{P \cdot r_{o} \cdot l \cdot {\sin\left( \frac{\theta}{2} \right)}}\quad{{where}:\theta}} = {{Change}\quad{in}\quad{angle}\quad{between}\quad{deck}\quad{plates}}}$r_(o) = Outside  radius  of  cylindrical  deckr_(o) = Force  from  differential  pressurel = Unit  length  of  plate${F_{n} = {{{l \cdot t \cdot \delta \cdot \frac{V_{i}^{2}}{2 \cdot r_{i}^{2}}}\left( {r_{o}^{2} - r_{i}^{2}} \right)\quad{{where}:F_{n}}} = {{{Normal}\quad{force}\quad{on}\quad{bar}\quad{from}\quad{rotation}t} = {{{thickness}l} = {{{unit}\quad{length}\delta} = {{{density}\quad{of}\quad{material}V_{i}} = {{{Velocity}\quad{{at}\quad}^{\prime\prime}{r_{i}}^{\prime\prime}r_{i}} = {{radius}\quad{on}\quad{inside}\quad{of}\quad{support}\quad{bar}{r = {{distance}\quad{from}\quad{center}\quad{of}\quad{TAD}}}}}}}}}}};{and}$$F_{t} = {{{2 \cdot T \cdot {\sin\left( \frac{\theta}{2} \right)}}\quad{{where}:F_{t}}} = {{{Force}\quad{per}\quad{unit}\quad{length}\quad{from}\quad{tension}T} = {{{Fabric}\quad{tension}\quad{per}\quad{unit}\quad{length}\theta} = {{Change}\quad{in}\quad{angle}\quad{between}\quad{deck}\quad{{plates}.}}}}}$43. An apparatus as defined in claim 33, wherein the first deck supportand the second deck support have a conical shape for directing gas flowbetween the cylindrical deck and the first and second hubs and whereinthe rotating tube shields the first bearing and the second bearing fromthe gas flow.
 44. An apparatus for through-air drying webs comprising: acylindrical deck having sufficient open space to permit air flowtherethrough, the cylindrical deck having a diameter; a supportstructure positioned to support the cylindrical deck, the supportstructure further being configured to rotate the cylindrical deck; andwherein the cylindrical deck and the support structure are configured tobe disassembled, the apparatus having a disassembled volume when beingshipped, the disassembled volume having a maximum dimension that is lessthan one half the diameter of the cylindrical deck.
 45. An apparatus asdefined in claim 44, wherein the cylindrical deck comprises a pluralityof individual deck plates that are attached to the support structure.46. An apparatus as defined in claim 45, wherein the support structurecomprises a first hub spaced from a second hub, each hub engaging anopposite end of the cylindrical deck, the support structure furthercomprising at least one internal deck support and a deck support ringthat provides support to the cylindrical deck in between the first endof the cylindrical deck and the second end of the cylindrical deck. 47.An apparatus for through-air drying webs comprising: a cylindrical deckhaving sufficient open space to permit air flow therethrough; a supportstructure positioned to support the cylindrical deck, the supportstructure comprising a first hub spaced from a second hub, each hubengaging an opposite end of the cylindrical deck; a support shaftconcentrically positioned with respect to the cylindrical deck, thesupport structure being configured to rotate on the support shaft; and afirst bearing positioned between the first hub and the support shaft anda second bearing positioned between the second hub and the supportshaft, each bearing being substantially in alignment with each end ofthe cylindrical deck.